Numerical Study on R32 Flow Condensation in Horizontally Oriented Tubes with U-Bends

In this paper, the flow condensation heat transfer characteristics of R32 in a horizontally oriented tube with a horizontal U-bend (HUB tube) and a horizontally oriented tube with a vertical U-bend (VUB tube) were numerically investigated. The volume of fluid (VOF) multiphase model with the mass tra...

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Bibliographic Details
Main Authors: Cao, Z. (Author), Chu, W. (Author), Mei, H. (Author), Wang, Q. (Author), Yan, G. (Author), Zhang, H. (Author)
Format: Article
Language:English
Published: MDPI 2022
Subjects:
Online Access:View Fulltext in Publisher
LEADER 02503nam a2200433Ia 4500
001 10.3390-en15134799
008 220718s2022 CNT 000 0 und d
020 |a 19961073 (ISSN) 
245 1 0 |a Numerical Study on R32 Flow Condensation in Horizontally Oriented Tubes with U-Bends 
260 0 |b MDPI  |c 2022 
856 |z View Fulltext in Publisher  |u https://doi.org/10.3390/en15134799 
520 3 |a In this paper, the flow condensation heat transfer characteristics of R32 in a horizontally oriented tube with a horizontal U-bend (HUB tube) and a horizontally oriented tube with a vertical U-bend (VUB tube) were numerically investigated. The volume of fluid (VOF) multiphase model with the mass transfer assumption by Lee is adopted to simulate the flow condensation behavior of R32, which are validated by well-known empirical correlations. The influence of structural parameters, mass flux and vapor quality on the heat transfer coefficient (HTC) and liquid film distribution is investigated. Meanwhile, the local liquid film thickness (LLFT) and local heat transfer coefficient (LHTC) are also depicted. The phase transition at the U-bend section is captured. Results show that the U-bend has remarkable disturbance on the flow pattern and LHTC due to the effect of centrifugal force where the LLFT is changed, inducing strong secondary flow. The LHTC is increased by a maximum of 8.47% and 11.86% in VUB tube and HUB tube, respectively, when compared to the case in a horizontally straight oriented tube at the same operating conditions. © 2022 by the authors. Licensee MDPI, Basel, Switzerland. 
650 0 4 |a Condensation 
650 0 4 |a Condensation heat transfer 
650 0 4 |a film thickness 
650 0 4 |a Film thickness 
650 0 4 |a Film-thickness 
650 0 4 |a Flow condensation 
650 0 4 |a Flow patterns 
650 0 4 |a heat transfer coefficient 
650 0 4 |a Heat transfer coefficients 
650 0 4 |a Heat transfer co-efficients 
650 0 4 |a Heat-transfer characteristics 
650 0 4 |a Liquid film thickness 
650 0 4 |a Liquid films 
650 0 4 |a Local heat transfer coefficient 
650 0 4 |a Local liquid 
650 0 4 |a Mass transfer 
650 0 4 |a R32 flow condensation 
650 0 4 |a Tubes (components) 
650 0 4 |a VOF model 
650 0 4 |a Volume of fluid model 
700 1 |a Cao, Z.  |e author 
700 1 |a Chu, W.  |e author 
700 1 |a Mei, H.  |e author 
700 1 |a Wang, Q.  |e author 
700 1 |a Yan, G.  |e author 
700 1 |a Zhang, H.  |e author 
773 |t Energies